WO2011085419A1

WO2011085419A1 - Rotor disk

Info

Publication number: WO2011085419A1
Application number: PCT/AT2011/000005
Authority: WO
Inventors: Manfred Hackl; Klaus Feichtinger; Gerhard Wendelin
Original assignee: Erema Engineering Recycling Maschinen Und Anlagen Gesellschaft M.B.H.
Priority date: 2010-01-14
Filing date: 2011-01-07
Publication date: 2011-07-21
Also published as: US9211546B2; BR112012002869A2; JP5343169B2; KR20120104488A; US20120024999A1; EP2442899A1; UA105205C2; AT508924B1; PT2442899E; AU2011206903B2; ES2430264T3; DK2442899T3; AT508924A4; PL2442899T3; AU2011206903A1; TW201134556A; MX2011010521A; RU2537494C2; CN102438737A; ZA201106211B

Abstract

The invention relates to a rotor disk (1) for inserting into a receiving container (2) for treating polymers, comprising a disk body (3), on the upper face (4) of which mixing and/or comminuting tools (5) can be provided and on the opposite lower face (6) of which a number of conveying ribs (7) extending from the inside out is provided, by means of which conveying ribs polymer particles can be conveyed outward during operation or which conveying ribs exert a force directed outward from the center (8) of the rotor disk (1) on the polymer particles caught by the conveying ribs (7) during operation. According to the invention, the thickness of the disk body (3) is reduced toward the outside.

Description

rotor disc

The invention relates to a carrier according to the preamble of the claim

1.

Such carriers are known in various embodiments from the prior art. These are usually arranged near the bottom of a receptacle or cutter compressor for the treatment and processing of thermoplastic polymers and essentially consist of a disc-shaped tool carrier, ^"at the top thereof mixing or stirring tools or crushing blade are arranged. In operation, the disc rotates and the If necessary, the tools grasp and, if necessary, chop up the plastic material in the container with simultaneous heating, and the material is thoroughly mixed and agitated so that a mixing drum is formed in the container.

Devices for processing polymers are basically also known from the prior art, e.g. from AT 375 867 B, AT 407 970 B or WO 93/18902. Due to the circulating tool carriers or tools, the treated plastic material is thrown against the container side wall by centrifugal force. A portion of this plastic material rises along the container side wall up and runs in the form of a Mischtrombe, but ultimately falls back into the container center. This results in the desired residence time of the treated plastic particles in the receptacle, so that the plastic material introduced into it well mixed, sufficiently heated by the friction forces occurring and, in the case of crushing acting on the plastic material tools, also sufficiently crushed.

However, it has been shown that not all of the container side wall thrown plastic material rises on this wall, but reaches a proportion down under the lowest tool or under the lowest forming the tool carrier disk. There, this Kunststoffgutanteil melt by friction uncontrolled.

Attempts have been made to avoid this disadvantage by attaching conveyor ribs to the underside of this disc. From the prior art, it is known in this respect, to install on the underside of the disc or the tool carrier straight and radial ribs, which serve plastic goods, which enters the area between the bottom of the cutting compressor and the bottom of the tool carrier, back to the outside to promote and remove from this area again. However, this measure has not completely satisfied. Especially with receptacles with large dimensions and a correspondingly large filling volume of several hundred kilograms of polymer material, also correspondingly large discs with large diameters must be used. On the one hand, these discs must be manufactured very precisely and, moreover, rotate very smoothly and regularly, since the distance between the disc and the bottom is only a few millimeters. In such a large-sized Schneidverdichtem very high demands are placed on the conveying effect of the ribs, since, as mentioned, in the container very much to be treated material is present, on the one hand to move and on the other hand pushes down strongly by its high weight and in the area between the Disc and the soil in it.

When upscaling such devices, it has been found that the delivery rate of the known discs, which still work well in smaller containers, is no longer sufficient for large containers to keep the material away from the delicate area. Also, the speed of the mixing tools to give the material an upward movement and to increase the residence time, can not be increased arbitrarily, since the increased friction again more heat would arise, which could lead to a local melting of the flakes.

Again and again then arrive polymer flakes in the outer area between the floor and disc and remain there permanently. As a result, the temperature in this area increases, the flakes agglomerate, become sticky and eventually melt, which causes only more flakes to accumulate. After some time, the disc begins to rattle and finally runs tight. It is thus desirable that, should a particle seep between the fins and the bottom of the container, it will be released as quickly as possible and then effectively removed from the critical region.

In addition, not only larger flakes, but also smaller dust particles get into the critical area below the disc, the dust particles penetrate much further towards the center of the disc and remain there. These fine polymer particles are then too heated and are isolated and trapped in the critical region.

Basically, this is problematic even with slices with a smaller diameter, since smaller rotational speeds, ie relatively low peripheral speeds, are used especially for heavy grinding stocks.

It is therefore an object of the present invention to provide a rotor disk, with which, especially at high filling volume and larger dimensions, effectively prevents polymer particles from getting into the critical region between the disc and the bottom of the receptacle or quickly and completely free and removed from this area. This object is solved by the characterizing features of claim 1, wherein it is provided that reduces the thickness of the disk body to the outside.

In this way, when processing and processing of plastic particles effectively causes even at high capacity and correspondingly high pressure down, both larger and coarser polymer flakes, which penetrate more only in the edge region of the disc, as well as finer dust particles, the very far can penetrate to the outside, whereby the critical area remains substantially permanently free of such particles.

In particular, this effectively prevents larger particles can wedge between the bottom and the disc and the disc is stuck. If particles nevertheless run the risk of remaining longer than intended in the small space between the bottom and the underside of the disk, they are more easily liberated and conveyed outwards by the thickness which reduces towards the outside.

As a result, an effective and homogeneous processing of the present in the receptacle polymer material is possible. In addition, standstill and repair times caused by a stall of the disc avoided. Also, the quality of the material to be treated improves, as local overheating or melting is prevented. Further advantageous embodiments of the invention are described by the dependent claims:

Thus, according to an advantageous development of the invention, it is provided that the thickness of the disk body decreases by at least 1 mm, preferably between 1.5 to 3.5 mm, this difference between the thickness of the disk body in the center or in an inner central area and measured at the outer edge. It has surprisingly been found that even with such minor changes a great improvement can be achieved.

A particularly advantageous embodiment provides that increases the height of the conveyor ribs in the direction of their course to the outside.

In particular, it is advantageous that the thickness of the disk body to the outside decreases to the same extent as the height of the conveyor ribs after externally increased or that the total thickness of the rotor disc remains constant and constant over its radius. Thus, a smooth running and effective promotion of the polymer particles from the critical area can be achieved.

Furthermore, it is advantageous if it is provided that the thickness of the disk body in an inner region is constant and decreases only from a distance from the center of the rotor disk, preferably from a distance of 60% of the radius, in particular between 60% and 70%. In the same way, it is advantageous if the height of the conveyor ribs in an inner region is constant and increases only from a distance from the center of the rotor disc, preferably from a distance of 60% of the radius, in particular between 60% and 70%. The dimensional changes lie only in an outer radial region, namely where the coarser flakes can barely penetrate. In this way, both coarse and fine particles are effectively transported to the outside.

According to a preferred embodiment, it is provided that the points or regions of the conveyor ribs which are furthest away from the upper side define or span a plane plane. Seen from the side, thus the total thickness of the carrier remains constant.

In this context, it is advantageous if it is provided that the upper side of the disk body is planar and / or that the plane is parallel to the upper side. Such a construction is also relatively easy to manufacture and very quiet.

A particularly effective rotor disk is characterized in that the underside of the disk body is beveled in the region in which its thickness decreases, and inclined to the top and / or to the plane, in particular at an angle of at most 3 °, in particular between 0, 4 and 0.6 °, is aligned. This results in a quasi-frustoconical design of the disc, which in turn was surprisingly found that only minor deviations and angular dimensions sufficient to achieve effective Entfrachtung.

A structurally simple embodiment provides that the reduction of the thickness of the disk body runs continuously in a plane, which also vortex formation can be avoided and the smoothness is increased.

However, a rotor disk is also effective if it is provided that the reduction of the thickness of the disk body is discontinuous or in stages, possibly a single stage. Whether a continuous or discontinuous reduction is more advantageous depends inter alia on the type, shape and dimensions of the material to be processed, for example, whether films, flakes or granules are recycled. It has surprisingly been found in this context that, in order to allow an even more effective promotion to the outside, it is advantageous if the conveyor ribs are concavely curved in the direction of the disc, whereby the fan effect increases even further. This feature synergistically supports the effect of reduced thickness and, surprisingly, additionally enhances the effect. If a particle penetrates further into the critical area, for example, if the treatment stops unexpectedly and the agitator has to be stopped, it is quickly removed.

It has proved to be advantageous if the curvatures are uniform and circular arc.

In this context, it is particularly advantageous to provide that the curvatures of all conveyor ribs are equal to each other. Such a rotor disk is structurally very simple to design.

If it is provided that at least two groups of conveyor ribs are provided, which start alternately at different distances from the center, namely from an inner central area and from an outer central area, the structural design of the disc is also facilitated, since very close together conveyor ribs in Interior of the disc can be avoided.

It has been found to be surprisingly advantageous for the conveying effect when the conveyor ribs are not aligned radially towards the center, but when the outer end portions of the conveyor ribs almost tangential to the edge of the rotor, in particular in an outer cutting angle between 0 ° and 25 °, preferably between 12 ° and 18 °, are aligned.

It is also advantageous if the inner starting areas of the conveyor ribs for

Center or to the inner central region or to the outer central region under internal angles of intersection or ß ₂ between 0 ° and 45 °, preferably between 15 ° and 30 °, are employed. It is advantageous if ß _{2 is} greater than.

Each cutting angle is measured in each case at the point of intersection or inlet point of the conveyor rib with or into the edge of the rotor disk or the inner central region or outer central region. In this case, the angle of intersection is in each case the angle between the tangent placed on the conveyor rib at this point of intersection and the tangent at this intersection point to the inner central area or outer central area.

During operation, the carrier rotates in the direction of the concave

Curvature. In this context, it is also advantageous if it is provided that the conveyor ribs have a substantially triangular cross-section, with a trained in the direction of straight and substantially perpendicular to the bottom conveying surface and a downstream of the direction beveled sloping planar flank surface. This ensures that if ponds get under the disc, they are quickly released and can be promoted out and it does not come to a stalling or braking of the disc.

In order to be able to influence the temperature of the plastic material to be processed via the conveyor disc, it is provided according to an advantageous further development that a cavity, optionally filled with or filled with a coolant, is formed in the disc body.

It is further provided according to the invention that the rotor disc is arranged in a cutting compactor with a small ground clearance. A particularly advantageous apparatus for the treatment and preparation of plastic goods provides a, in particular evacuable, receptacle, wherein the carrier according to the invention is arranged close to and parallel to the bottom surface. The rotor disc is advantageously carried by a substantially vertically aligned shaft and driven, so that the plastic material located in the receptacle receives a circulating movement about the axis of the shaft.

In a particularly advantageous embodiment, the distance between the rotor disk, namely between the outermost, disk-distal points or edges of the conveyor ribs, and the bottom surface of the receptacle is less than the thickness of the disk body, preferably in the range between 3 and 15 mm, preferably between 4 to 8 mm.

Further advantages and embodiments of the invention will become apparent from the description and the accompanying drawings.

The invention is illustrated below with reference to a particularly advantageous embodiment in the drawings and will be described with reference to the drawings, for example.

Fig. 1 shows the rotor according to the invention from below.

FIG. 2 shows a sectional view through the center of the disk according to FIG. 1. FIG. 3 shows an enlarged view of the section according to FIG. 2.

FIG. 4 shows a detail detail of the right side of the section according to FIG. 2 or FIG. 3. FIG. 5 shows the partial section BB of FIG. 1.

FIG. 6 shows detail view A of FIG. 1.

Fig. 7 shows a section of a receptacle with disc arranged therein.

In Fig. 1, a particularly effective and advantageous carrier 1 is shown by way of example, Fig. 1, the rotor disc 1 from below, that is seen in operation from the container bottom 17, shows. In practice, such carriers 1 are usually used in large-volume receptacles 2, in which there is a lot of polymer material with a correspondingly high weight. Accordingly, high pressure is applied to the rotor disk 1. The diameter of such a rotor disk 1 is in these cases in the range of about 2 m and more.

The rotor disk 1 has a disk body 3, on the top side 4 of which mixing and / or comminution tools 5 can be arranged. On the opposite bottom 6 of the disk body 3, a number of extending from the inside to the outside conveyor ribs 7 is arranged. All conveyor ribs 7 are concavely curved in the direction of the disc 1, wherein the curvatures are uniformly circular arc. The radius of curvature of the conveyor ribs 7 is less than the radius of the rotor disc 1 and is about 65% thereof. In addition, the curvatures of all conveyor ribs 7 are almost equal to each other.

There are two groups of conveyor ribs 7 are provided, namely longer and shorter, which are arranged alternately to each other. The longer conveyor ribs 7 start at an inner circular central region 14 whose radius is about 30% of the radius of the rotor disc 1. The shorter conveyor ribs 7 start at an outer central region 15 whose radius is about 50% of the radius of the rotor disk 1. All conveyor ribs 7 run continuously to the outermost edge of the rotor disk 1 and the disk body. 3

The conveyor ribs 7 are not aligned radially to the center 8 of the rotor disc 1.

Thus, the outer end portions of all conveyor ribs 7 are aligned almost tangentially to the outer edge of the rotor and in an outer intersection angle α of about 14 °, measured at the inlet point of the conveyor rib 7 to the edge or circumference, between the set to the outermost edge tangent and the tangent to the conveyor rib 7, where the conveyor rib 7 touches the outermost edge or perimeter.

The inner initial portions of the longer conveyor ribs 7 are internal

Central region 14 at a first inner intersection angle βτ of about 15 ° employed, measured in each case at the inlet point of the conveyor rib 7, between the tangent to the inner central region 14 and the tangent to the conveyor rib 7, where this or the conveying rib 7 touches the inner central region 14.

The inner initial regions of the shorter conveyor ribs 7 are made to the outer central region 15 at a second inner intersection angle ß ₂ of about 35 ° to 40 °, measured at the inlet point of the conveyor rib 7, between the tangent to the outer central region 15 and the tangent to the conveyor rib 7, where this or the conveying rib 7 touches the outer central region 15.

It is advantageous if ß _{2 is} greater than fr.

In the contact area to the inner central region 14 and the outer central region 15, the conveyor ribs 7 are tapered or ending.

In operation, both large and small polymer particles can be conveyed outward with such conveyor ribs 7 or a force directed outwards from the center 8 of the rotor disk 7 is exerted on the particles detected by the conveyor ribs 7. The conveying effect is usually effected by the mechanical action of the conveyor ribs 7 on the polymer particles, since the treatment is usually carried out in vacuo. In the same way, however, a treatment under ambient pressure is possible, which in addition to the mechanical contacts between conveyor ribs 7 and polymer particles also flow effects occur.

2, 3 and 4, the rotor disc 1 is shown in a cross section through the center 8. At the top of the disk body 3 facing the container during operation, mixing and / or comminution tools 5 can be arranged. In the present embodiment, such tools are not shown. The mixing and / or crushing tools 5 may be blades, knives or the like. These capture the polymer particles and bring them into a rotating motion, which forms a Mischtrombe in the container. In addition, the particles are heated and kept in constant mixing, so that even at elevated temperatures, gluing or sticking is avoided. Optionally, there is also a shredding or crushing of larger granules.

At the bottom 6 of the disk body 3, the conveyor ribs 7 are arranged. The thickness of the disk body 3 in an inner region 9 is constant and constant. This inner region 9 extends to approximately two-thirds of the radius of the rotor disc 1. From a certain distance 18 from the center 8 of the rotor 1, the thickness of the disk body 3 is then reduced. In the present example, the radial distance 18 is about 68% of the radius of the Rotor disc 1. Also from this radial distance 18, the height of the conveyor ribs increases towards the outside Accordingly, while the height of the conveyor ribs 7 in the inner region 9 is constant and constant.

It can be seen from FIGS. 2 to 4 that the thickness of the disk body 3 decreases only slightly, in the present exemplary embodiment by only 2 mm. In the same way and to the same extent, the height of the conveyor ribs 7 increases according to their course to the outside, so that the total thickness of the rotor 1 over its entire radius is the same and constant. In this outer region, only the distance between the disk body 3 or the underside 6 and the uppermost points of the conveyor ribs 7 is greater or the area between the conveyor ribs 7 is slightly higher.

The tops 4 or regions of the conveyor ribs 7 which are furthest from the upper side 4 form a flat plane 10, this plane 10 being aligned parallel to the also flat upper side 4 of the disk body 3.

The reduction of the thickness of the disk body 3 in the present example runs continuously or over an inclined plane. The underside 6 of the disk body 3 is chamfered in the outer region, in which its thickness decreases, and upwardly inclined to the upper side 4 at an angle γ of about 0.5 °. The rotor disk 1 or the disk body 3 thus has in some way the shape of a truncated cone with a flattened outermost peripheral edge.

According to another possible embodiment, the thickness of the

Disc body 3 also discontinuously or reduce over steps, which brings advantages in certain recyclates.

Furthermore, it is provided that at least one cavity 13 through which a coolant flows is formed in the interior of the disk body 3, via which a cooling of the disk can take place.

In Fig. 5 is a cross section through a conveyor rib 7 is shown. Each conveyor rib 7 has a substantially triangular cross-section, with a plane oriented in the direction of planar and substantially perpendicular to the bottom 6 aligned conveying surface 11 and downstream of the running direction at an angle δ between 10 ° and 35 °, in particular about 15 ° sloping sloping flat flank surface 12.

In Fig. 6 is a view of a conveyor rib 7 is shown obliquely from the side of the rotor disc 1. It can be seen that the flank surface 12 does not transition continuously, directly or at an acute angle, but rather via an edge or step 20 into the underside 6. However, the transition can also be made without level 20. FIG. 7 shows a rotor disk 1 according to the invention in operation, namely inserted into a device for the treatment and processing of plastic material. In Fig. 7, the lower left portion of such a device is shown. The rotor disk 1 is used in an evacuable receptacle 2, which has a flat horizontal floor surface 17 and vertical side walls 18. The rotor disk 1 is arranged very close to the ground and parallel to the bottom surface 7 and is supported by a substantially vertically aligned shaft 19 and is also driven by this shaft 19. By the rotation of the rotor disc 1, in particular by the mixing tools 5, the material contained in the receptacle 2 is moved and undergoes, inter alia, a circulation movement about the axis of the shaft 19th

The distance 21 between the rotor disk 1, namely between the outermost, disk-distal points or edges of the conveyor ribs 7 or the plane 10, and the bottom surface 17 is relatively small and is in the range between about 5 to 6 mm. In Fig. 6, the distance 21 between the bottom surface 17 and the rotor disc 1 is shown schematically and not to scale. The disk, with a diameter of about 2000 mm, usually rotates at a speed of about 10 to 300 revolutions per minute, e.g. 20 to 150 rpm.

A particularly advantageous embodiment of a device has an evacuable receptacle 2 with a circular cross-section and with a vertical axis, in which the plastic material to be processed, in particular a thermoplastic type, e.g. PET (polyethylene terephthalate), in the form of ground material from bottles or bottle preforms, films, flakes, etc. is introduced from above through an insertion opening. At this opening, if the material to be processed must be processed under vacuum, a lock is connected, the lock chamber is closed by two slides, which can be moved by double-acting cylinders back and forth. At the top of the lock, there is connected a hopper into which the material to be processed is fed batchwise or continuously by means not shown, e.g. a conveyor belt is introduced. To the lock chamber an evacuation line is connected, which leads to an evacuation device. Another evacuation line leads from the receptacle 2 to the evacuation device.

The receptacle 2 has vertical side walls 18 and a horizontal bottom 17. Near the bottom 17, a tool carrier is arranged, which is formed by a horizontal circular rotor 1, which sits on a floor 17 vacuum-tight passing through shaft 19, of a motor for rotation is driven in the direction of the arrow. The disc 1 carries on its surface 4 more to the Scope of the rotor disc 1 at regular intervals distributed tools 5, which act upon the rotation of the disc 1 on the located in the container 2 Kunststoffgut. As a result, this plastic material is driven on the one hand to circulate about the axis 19, on the other hand, the centrifugal force seeks to move the plastic material in the radial direction to the side wall 18. The result is a Mischtrombe such that a proportion of the plastic rises good along the side wall 18, reaches a culmination point in this circulation and finally falls back into the area of the container axis. However, not all of the plastic goods take part in this rising, because a portion of the plastic material thrown off the disk 1 seeks to get into the critical space below the disk 1, in particular if there is a lot of material in the container.

To alleviate this somewhat, the disc 1 carries in the present case a plurality, distributed around the disc circumference at regular intervals arranged inclined blades. These blades impart a preferred upward movement to the plastic material thrown off the disk 1 by the tools 5 and thus to some extent prevent the processing of the material in the container 2 from causing plastics material components to enter the space below the disk 1 of the tool carrier.

However, this effect is optimized only when the conveyor ribs 7 according to the invention are arranged on the underside 4 of the pane 1, which are arranged such that the plastic material reaching or reaching the critical area is conveyed in the direction of the side wall 18. The so moved outward plastic material is then detected by the blades and conveyed back up.

Claims

claims:

1. rotor disc (1) for insertion into a receptacle (2) for the treatment of polymers, with a disc body (3), at the top (4) mixing and / or

Crushing tools (5) are providable and on the opposite underside (6) a number of extending from inside to outside conveyor ribs (7) is provided with which in operation polymer particles are conveyed to the outside or in operation on the of the conveyor ribs ( 7) exert a detected polymer particles from the center (8) of the rotor disc (1) outwardly directed force, characterized in that the thickness of the disc body (3) decreases towards the outside.

2. rotor disc according to claim 1, characterized in that the thickness of the disc body (3) by at least 1 mm, preferably between 1, 5 to 3.5 mm, decreases.

3. rotor disc according to claim 1 or 2, characterized in that increases the height of the conveyor ribs (7) in the direction of their course to the outside.

4. rotor according to one of claims 1 to 3, characterized in that the thickness of the disk body (3) decreases to the outside to the same extent, as the height of the conveyor ribs (7) increases towards the outside.

5. rotor according to one of claims 1 to 4, characterized in that the total thickness of the rotor disc (1) over its radius is the same and constant.

6. rotor disc according to one of claims 1 to 5, characterized in that the thickness of the disc body (3) in an inner region (9) is constant and from a distance (18) from the center (8) of the rotor disc (1), preferably from a distance (18) of 60% of the radius, in particular between 60% and 70%, reduced and / or that the height of the conveyor ribs (7) in an inner region (9) is constant and from a distance (18) from the center (8) of the rotor disc (1), preferably from a distance (18) of 60% of the radius, in particular between 60% and 70%, increased.

7. Rotor according to one of claims 1 to 6, characterized in that the top (4) farthest points or areas of the conveyor ribs (7) define a plane (10) or span.

8. rotor according to one of claims 1 to 7, characterized in that the upper side (4) of the disk body (3) is plane and / or that the plane (10) parallel to the upper side (4).

9. A rotor according to any one of claims 1 to 8, characterized in that the underside (6) of the disc body (3) in the region in which its thickness is reduced bevelled and the top (4) and / or to the plane ( 10) inclined, in particular at an angle γ of a maximum of 3 °, in particular between 0.4 ° and 0.6 °, is aligned.

10. rotor according to one of claims 1 to 9, characterized in that the reduction of the thickness of the disk body (3) is continuous.

11. A rotor according to any one of claims 1 to 10, characterized in that the reduction of the thickness of the disk body (3) discontinuously or in stages, optionally a single step, runs.

12. rotor according to one of claims 1 to 11, characterized in that the conveyor ribs (7) are concavely curved in the rotational or running direction.

13. rotor according to one of claims 1 to 12, characterized in that the curvatures of all conveyor ribs (7) are equal to each other and / or the curvatures are uniform, preferably circular arc, are.

14. A rotor according to any one of claims 1 to 13, characterized in that at least two groups of conveyor ribs (7) are provided which alternately at different distances from the center (8), namely from an inner central region (14) and from an outer Central area (15), begin.

15. A rotor according to one of claims 1 to 14, characterized in that the outer end portions of the conveyor ribs (7) almost tangentially to the edge of the rotor disc (1), in particular at outer cutting angles between 0 ° and 25 °, preferably between 12 ° and 18 °, and / or that the inner initial regions of the conveyor ribs (7) to the inner central region (14) and to the outer central region (15) of first and second inner intersection angles ß, or ß ₂ between 0 ° and 45 °, preferably between 15 ° and 30 °, the second inner cutting angles β _{2 are} preferably larger than the first inner cutting angles β-, the intersecting angles between the tangents placed on the conveyor ribs (7) and the tangents placed on the edge of the rotor disk (1) or on the inner central region (14) or outer central region (15), at the intersection of these tangents the inlet points of the conveyor ribs (7) are measured.

16. Carrier according to one of claims 1 to 15, characterized in that the conveying ribs (7) have a, in particular substantially triangular, cross-section, with a running direction formed in the straight and substantially perpendicular to the bottom (6) aligned conveying surface (11). and a flank surface (12) sloping downstream of the running direction, the flank surface (12) being oriented at an angle δ to the underside (6) of 10 ° to 35 °, in particular of approximately 15 °.

17. A rotor according to one of claims 1 to 16, characterized in that in the disk body (3) at least one, optionally filled with a coolant or durchströmbarer, cavity (13) is formed.

18. Device for the treatment and preparation of plastic goods, with a, in particular evacuable, receptacle (2) having a flat bottom surface (17) and side walls (18), wherein close to and parallel to the bottom surface (17) has a rotor (1 ) is rotatably arranged according to one of claims 1 to 17, wherein the rotor disc (1) in particular by a substantially vertically aligned shaft (19) is supported and driven, so that in the receiving container (2) located plastic material is movable.

19. The apparatus according to claim 18, characterized in that the distance between the outermost, most disk-distal points or edges of the conveyor ribs (7) or the plane (10) and the bottom surface (17) is less than the thickness of the disk body (3). and preferably between 3 and 15 mm, preferably between 4 and 8 mm.